US4374068AExpiredUtility

Process for hydroxyalkylation of cyanoethylanilines

43
Assignee: MILLIKEN RES CORPPriority: Oct 15, 1981Filed: Oct 15, 1981Granted: Feb 15, 1983
Est. expiryOct 15, 2001(expired)· nominal 20-yr term from priority
C07C 255/00
43
PatentIndex Score
2
Cited by
3
References
12
Claims

Abstract

A process is provided for hydroxyalkylation of cyanoethylanilines, which comprises reacting an alkylene oxide of the formula: ##STR1## wherein R 1 is selected from H, Cl, Br, OH, a lower alkyl group containing from 1 to about 4 carbon atoms, or phenyl with a cyanoethyl aniline in a molar ratio of from about 1:1 to about 2:1 in a reaction medium at a temperature of from about 40° C. to about 130° C. in the presence of an acid catalyst provided in an amount sufficient to catalyze said reaction to thereby provide the corresponding hydroxyalkylated cyanoethyl aniline.

Claims

exact text as granted — not AI-modified
What is claimed is: 
     
       1. A process for hydroxyalkylation of cyanoethylanilines which comprises reacting an alkylene oxide of the formula: ##STR6## wherein R 1  is selected from H, Cl, Br, OH, a lower alkyl group containing from 1 to about 4 carbon atoms, or phenyl with a cyanoethylaniline in a molar ratio of from about 1:1 to about 2:1 in a reaction medium at a temperature of less than 100° C. in the presence of an acid catalyst provided in an amount sufficient to catalyze said reaction to thereby provide the corresponding hydroxyalkylated cyanoethylaniline. 
     
     
       2. The process of claim 1 wherein said cyanoethylanilines are represented by the following structural formula: ##STR7## wherein R 2  is selected from H, Cl, Br, OH, a lower alkyl group containing from 1 to about 4 carbon atoms, or phenyl; and R 3 , R 4  and R 5  are each independently selected from H, a lower alkyl group containing from 1 to about 4 carbon atoms, halogen, NO 2 , OH, a lower alkoxy group containing from 1 to about 4 carbon atoms, and NHCOR 6  where R 6  is H or a lower alkyl group containing from 1 to about 4 carbon atoms. 
     
     
       3. The process of claim 1 wherein said reaction is performed for from about 0.2 to about 8 hours. 
     
     
       4. The process of claim 1 wherein said reaction is performed in the absence of a solvent. 
     
     
       5. The process of claim 1 wherein said reaction is performed in the presence of a solvent selected from water, cycloaliphatic ethers and high boiling hydrocarbons. 
     
     
       6. The process of claim 1 wherein said acid catalyst is an organic acid. 
     
     
       7. The process of claim 6 wherein said organic acid is selected from acetic, formic, propionic, paratoluenesulfonic or methanesulfonic acids. 
     
     
       8. The process of claim 7 wherein said acid is acetic acid. 
     
     
       9. The process of claim 1 wherein said acid catalyst is present in an amount of from about 1 percent to about 30 percent by weight. 
     
     
       10. The process of claim 1 wherein said acid catalyst is a Lewis acid. 
     
     
       11. The process of claim 1 wherein said Lewis acid is zinc chloride. 
     
     
       12. The process of claim 1 wherein said acid catalyst is a mineral acid catalyst.

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